The disclosure relates to honeycomb extrusion body devices, and more particularly to honeycomb extrusion body devices useful for one or more of heat exchange, mixing, and similar processes, and particularly for mixing.
The present inventors and/or their colleagues have previously developed processes for forming serpentine channels within a honeycomb extrusion body and devices using such channels beneficially for various fluid processing needs. Generally in such devices, with reference to prior at
Some details of how plugs or seals 46 help form the path 32 are shown in the cross-sectional views of prior art
The present inventors have recognized that it would be desirable to improve the utility of the honeycomb extrusion body devices for any combination of heat exchange and mixing and relating processes, but particularly for mixing, while maintaining ease of fabrication. An embodiment of the present invention addressing this need takes the form of a honeycomb extrusion body having multiple cells extending along a common direction from a first end of the body to a second end and separated by cell walls, the body having at least one fluid path defined within a plurality of said cells, the fluid path having including at least one direction-reversing bend, at which bend the path on entering the bend includes two or more separate cells and at which the path on leaving the bend includes only one cell. The body desirably includes first and second input ports, the first fluid input port being in fluid communication with one of the two or more separate cells and the second fluid input port being in fluid communication with another of the two or more separate cells. The flow path provided in such a body has surprisingly good mixing characteristics while being relatively easy to manufacture.
These features, as well as others described herein below, provide increased heat exchange performance, increased mixing performance, increased preservation of emulsions, and the like, by inducing secondary flows within the cells in which the fluid path lies.
Additional features and advantages will be set forth in the detailed description which follows, and in part will be readily apparent to those skilled in the art from that description or recognized by practicing the embodiments as described herein, including the detailed description which follows, the claims, as well as the appended drawings.
It is to be understood that both the foregoing general description and the following detailed description are merely exemplary, and are intended to provide an overview or framework to understanding the nature and character of the claims. The accompanying drawings are included to provide a further understanding, and are incorporated in and constitute a part of this specification. The drawings illustrate one or more embodiment(s), and together with the description serve to explain principles and operation of the various embodiments.
Reference will now be made in detail to the present preferred embodiments, examples of which are illustrated in the accompanying drawings. Whenever possible, the same reference numerals will be used throughout the drawings to refer to the same or like parts.
Bends 14 of the type disclosed herein can also be used to laminate multiple streams as shown in the cross-section of
The full utility of these structures can be better appreciated from the plan view diagrams of a portion of a honeycomb body U-bend mixer shown in
In both
The methods and/or devices disclosed herein provide an easily manufactured two-into-one or many-into-one fluid mixer within the larger structure of a honeycomb-body heat exchanger or heat-exchanging reactor or mixer, with the option of providing a laminating mixer arrangement where multiple subsets of the many streams of a many-to-one mixer are of the same type. The methods and/or devices disclosed herein are generally useful in performing any process that involves mixing, separation, extraction, crystallization, precipitation, or otherwise processing fluids or mixtures of fluids, including multiphase mixtures of fluids—and including fluids or mixtures of fluids including multiphase mixtures of fluids that also contain solids—within a microstructure. The processing may include a physical process, a chemical reaction defined as a process that results in the interconversion of organic, inorganic, or both organic and inorganic species, a biochemical process, or any other form of processing. The following non-limiting list of reactions may be performed with the disclosed methods and/or devices: oxidation; reduction; substitution; elimination; addition; ligand exchange; metal exchange; and ion exchange. More specifically, reactions of any of the following non-limiting list may be performed with the disclosed methods and/or devices: polymerisation; alkylation; dealkylation; nitration; peroxidation; sulfoxidation; epoxidation; ammoxidation; hydrogenation; dehydrogenation; organometallic reactions; precious metal chemistry/homogeneous catalyst reactions; carbonylation; thiocarbonylation; alkoxylation; halogenation; dehydrohalogenation; dehalogenation; hydroformylation; carboxylation; decarboxylation; amination; arylation; peptide coupling; aldol condensation; cyclocondensation; dehydrocyclization; esterification; amidation; heterocyclic synthesis; dehydration; alcoholysis; hydrolysis; ammonolysis; etherification; enzymatic synthesis; ketalization; saponification; isomerisation; quaternization; formylation; phase transfer reactions; silylations; nitrile synthesis; phosphorylation; ozonolysis; azide chemistry; metathesis; hydrosilylation; coupling reactions; and enzymatic reactions.
This application claims the benefit of priority under 35 USC 119(e) of U.S. Provisional Application Ser. No. 61/265,354 filed on Nov. 30, 2009.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US10/57725 | 11/23/2010 | WO | 00 | 4/24/2012 |
Number | Date | Country | |
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61265354 | Nov 2009 | US |